An experimental and kinetic modeling study on the Ni-catalyzed conversion of methane under oxidative and reforming conditions is presented. The numerical model is based on a surface reaction mechanism consisting of 52 elementary-step like reactions with 14 surface and six gas-phase species. Reactions for the conversion of methane with oxygen, steam, and CO2 as well as methanation, water-gas shi...

This paper presents the results of mathematical models’ development for hydrotreating reactor, stripping ??lumn, absorbers and furnace which are basic units block in catalytic reforming unit. Since these objects modeling unit Atyrau refinery operate conditions insufficiency fuzziness initial information, their models developed on basis a systematic approach, using available information differen...

Fuel cell powered electric cars using on-board methanol or hydrocarbon reforming to produce a hydrogenrich gas represent a low-emissions alternative to gasoline internal combustion engines (ICE) with well-towheel efficiencies of 17 %. For the overall methanol process, a simplified model of the reaction network consisting of the total oxidation of methanol, the reverse water-gas shift reaction, ...

The partial oxidation of methane to synthesis gas was investigated in a novel type of perm selective membrane reactor using Perowskite hollow fibers. The operating behaviour of this membrane reactor integrating the process steps selective separation of oxygen from air, selective O2 transfer in the membrane and oxidation of methane with simultaneous steam reforming was investigated theoretically...

A clean stream of alkanes from renewable biomass resources is obtained through aqueous-phase reforming in a single reactor. Alkanes are produced from biomass-derived sorbitol through a bifunctional pathway (see scheme) that involves the dehydration of sorbitol on acid sites (SiO2/Al2O3) and hydrogenation of intermediates on a metal catalyst under a H2 atmosphere. Hydrogen is produced from sorbi...

a mathematical model for commercial naphtha catalytic reformer of tehran refinery was developed. this model includes three sequencing fixed beds of pt/al2o3 catalyst at the steady state condition using detailed kinetic scheme involving 26 pseudo-components connected by a network of 47 reactions, in the range of c6 to c9 hydrocarbons. the reaction network consisted dehydrogenation, hydrogenation...

Therefore, the RWGS reaction was also included in the analysis. As will be seen this reaction plays an extremely important role, limiting the amount of hydrogen that can be produced at high pressures. The reforming reaction was carried out at various pressures and temperatures and, for the first time, a tradeoff in hydrogen production due to the effect of pressure on thermodynamic equilibrium a...

The production of syngas from the pyrolysis-catalytic reforming processed municipal solid waste in form refuse derived fuel has been investigated experimentally using a two-stage fixed bed reactor with 10 wt% Ni–Al2O3 catalyst. gases used were combination steam and carbon dioxide (dry reforming). main focus research was to manipulate H2:CO ratio for targeted end-use applications by optimizing p...

Steam reforming of ethanol in the membrane reactor using the Pd77Ag23 membrane was evaluated in Ni/CeO2 and Co/CeO2 at atmospheric pressure. At 673 K, the H2 yield in the Pd77Ag23 membrane reactor over Co/CeO2 was found to be higher than that over Ni/CeO2, although the H2 yield over Ni/CeO2 exceeded that over Co/CeO2 at 773 K. This difference was owing to their reaction mechanism. At 773 K, the...